Selective separation and recovery of strontium from seawater reverse osmosis brine using sequential oxalate precipitation and ion exchange

Seawater desalination effectively produces fresh water, yet brine byproducts raise significant environmental concerns. Strontium, a valuable resource in brine, is increasingly sought after due to diminishing terrestrial mineral sources. However, its recovery is challenging because strontium ion (Sr 2+ ) and calcium ion (Ca 2+ ) exhibit similar physicochemical behaviors in the aqueous phase, necessitating advanced recovery technologies. This study proposes an integrated recovery process for seawater reverse osmosis (SWRO) brine combining oxalate-based precipitation and ion exchange. In the pretreatment stage, NaOH and oxalate were employed to sequentially remove magnesium and calcium interferences. Specifically, oxalate addition at a 1.6 molar ratio relative to Ca 2+ preferentially precipitated calcium, drastically increasing the [Sr 2+ ]/[Ca 2+ ] ratio from 0.016 to 2.5, indicating a notable enhancement in Sr 2+ relative to Ca 2+ . For the enrichment of Sr 2+ from the pretreated solution, an ion-exchange column was employed. Two consecutive concentration cycles yielded a Sr-enriched solution exceeding 4 g/L. A post-IEX Ca 2+ removal step further reduced residual calcium, achieving a maximum [Sr 2+ ]/[Ca 2+ ] ratio of 28.6, with a Sr 2+ concentration of approximately 2 g/L. These results demonstrate that an integrated process using sequential oxalate-based precipitation and ion exchange achieves high efficiency in Ca 2+ removal, enhancing the overall feasibility of the Sr 2+ recovery process.

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Publication Details

Journal
Desalination and Water Treatment
Published
2026-03-21
DOI
https://doi.org/10.1016/j.dwt.2026.101734
Primary Topic
Membrane Separation Technologies
Type
article
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article

Selective separation and recovery of strontium from seawater reverse osmosis brine using sequential oxalate precipitation and ion exchange

Jeong-Ki Moon, Won Suk Lee, Hyuk-Jun Kwon, Sangki Choi et al.
Desalination and Water Treatment
Membrane Separation Technologies
article

Selective separation and recovery of strontium from seawater reverse osmosis brine using sequential oxalate precipitation and ion exchange

Jeong-Ki Moon, Won Suk Lee, Hyuk-Jun Kwon, Sangki Choi, Taebum Ahn
article en

Abstract

Seawater desalination effectively produces fresh water, yet brine byproducts raise significant environmental concerns. Strontium, a valuable resource in brine, is increasingly sought after due to diminishing terrestrial mineral sources. However, its recovery is challenging because strontium ion (Sr 2+ ) and calcium ion (Ca 2+ ) exhibit similar physicochemical behaviors in the aqueous phase, necessitating advanced recovery technologies. This study proposes an integrated recovery process for seawater reverse osmosis (SWRO) brine combining oxalate-based precipitation and ion exchange. In the pretreatment stage, NaOH and oxalate were employed to sequentially remove magnesium and calcium interferences. Specifically, oxalate addition at a 1.6 molar ratio relative to Ca 2+ preferentially precipitated calcium, drastically increasing the [Sr 2+ ]/[Ca 2+ ] ratio from 0.016 to 2.5, indicating a notable enhancement in Sr 2+ relative to Ca 2+ . For the enrichment of Sr 2+ from the pretreated solution, an ion-exchange column was employed. Two consecutive concentration cycles yielded a Sr-enriched solution exceeding 4 g/L. A post-IEX Ca 2+ removal step further reduced residual calcium, achieving a maximum [Sr 2+ ]/[Ca 2+ ] ratio of 28.6, with a Sr 2+ concentration of approximately 2 g/L. These results demonstrate that an integrated process using sequential oxalate-based precipitation and ion exchange achieves high efficiency in Ca 2+ removal, enhancing the overall feasibility of the Sr 2+ recovery process.

Desalination and Water TreatmentVol. 326
Ulsan College (KR), Research Institute of Industrial Science and Technology (KR), Gyeongbuk Marine Bio-Industry Research Institute (KR), Pusan National University (KR)
Life below water
Openalex Percentile: Top 13%
Membrane Separation Technologies
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